Laserfiche WebLink
i <br /> i <br /> k9 KLEINFELDER <br /> 3 BACKGROUND <br /> i <br /> The Disco Remediation Area is the site of a former gasoline service station located on <br /> . the southern portion of the Del Monte site. The Disco Remediation Area was operated <br /> as a service station until Del Monte purchased the property in 1976. Del Monte never <br /> operated the service station. <br /> Three 10,000-gallon underground storage tanks (USTs) were identified on the Disco <br /> site. The USTs were removed in 1985. During the removal of the USTs impact to soil <br /> beneath the tanks was noted. The soil was excavated and aerated on the site and <br /> backfilled into the excavation. In 1991, a soil and groundwater investigation began. <br /> That investigation included a soil gas survey, seven soil borings, and installation of <br /> eight monitoring wells. The results showed concentrations of Total Petroleum <br /> Hydrocarbon as gasoline (TPH-g) in the soil at depths ranging from 55 feet to 75 feet <br /> below the ground surface (bgs), and also in the groundwater. <br /> In February 1995, a soil vapor extraction and air sparging system (SVEIAS) was <br /> installed and operated at the site (CH2M Hill, 1995). An estimated 8,787 pounds of <br /> TPH-g were removed while the system was in operation up to November 1995. The <br /> SVEIAS was shut down due to rising groundwater levels above the SVE systems <br /> screened level. The rising water levels were caused primarily by the shutdown of not <br /> only three Del Monte production wells, but also reportedly by the shutdown of numerous <br /> city municipal wells in the area. <br /> The main contaminants are TPH-g, benzene, toluene, ethylbenzene, xylene, and 1,2- <br /> DCA. The site is currently being monitored on a quarterly basis. In 2003 Kleinfelder <br /> replaced the soil vapor extraction system, and air sparge/ozone injection systems were <br /> installed to further remediate the plume. In general, the source area (actual Disco site) <br /> began active remediation in May 2003 using the thermal oxidizer. In June, that portion <br /> 4 of the remediation system.began operating full time. In July, the vapor extraction unit <br /> was converted from thermal oxidizer to catalytic oxidizer, and was operating continually. <br /> Regarding the down gradient edge of the plume, the ozone injection system began <br /> consistent and continuous operation in September 2003 except during times of system <br /> maintenance and enhancements. <br /> a <br /> 12280.M0NIST06R070/CD:Iv Page 6 of 14 <br /> 0 2006 Kleinfelder, Inc. February 16,2006 <br />